Bioactive peptides, uses thereof and process for the production of same

ABSTRACT

Novel bioactive peptide compositions and process for producing the same and the use of such compositions for enhancing the growth of warm blooded animals and fish is disclosed.

FIELD OF THE INVENTION

This invention relates to novel bioactive peptide compositions whichenhance the growth of animals, a process for the preparation of same andthe use of such compositions for enhancing the growth of warmbloodedanimals and fish.

BACKGROUND OF THE INVENTION

It is well known that porcine and bovine plasma protein can be used infeed formulations for warm blooded animals to improve health, growth andgeneral performance. However, the need for a replacement for such plasmaprotein is of great importance. The cost of plasma protein continues toincrease as foreign and domestic demand increases. In addition,inadequate supply of plasma protein is a frequent problem. Also, due toconcern of contamination of host animals through the feeding of plasmaprotein there is becoming a further need for a non-plasma product whichcan be utilized in those formulations where plasma protein is either notavailable or its use barred.

In addition, it is well known that protein hydrolyzates prepared byreaction of selected protein materials with at least one proteolyticenzyme can also be used in feed formulations. Such compounds aregenerally in such amounts as to maximize its content in the feedformulation without having a negative effect on the host. Suchhydrolyzates provided a replacement for fish meal as a protein sourceand thus while providing nutritional values provided no other benefit inthe growth of the host.

Thus there is presently experienced a need for a suitable replacementfor plasma as an ingredient of feed formulations as well as the need toachieve growth enhancement for host animals.

SUMMARY OF THE INVENTION

The aforementioned need is met by the present invention by providing abioactive peptide composition which not only provides an alternative toplasma products but also serves to enhance the growth of both animalsand fish.

According to the present invention a bioactive peptide composition isproduced by the enzymatic hydrolysis of a protein using the proteolyticenzyme derived from cod, specifically the stomachs of Atlantic cod.

The present invention is based upon the discovery that the peptideproduct obtained through enzymatic hydrolysis of a protein source withthe pepsin enzyme derived from the stomach of Atlantic cod can be usedas a substitute for plasma protein in achieving growth enhancement ofwarm blooded animals.

In a first aspect of the present invention there is provided novelanimal feed compositions which enhance growth.

In addition, the present invention is also based on the furtherdiscovery that such peptide products can be used at low levels toenhance the growth of fish.

Accordingly, in one aspect of the present invention there is provided anovel peptide product which is useful for enhancing the growth of warmblooded animals and fish.

In another aspect of this invention there is provided a process for theproduction of growth enhancing peptides from a protein source.

In another aspect of this invention there is provided a novel processfor enhancing the growth of warm blooded animals and fish.

Other aspects, objects and the several advantages of this invention willbe apparent from the foregoing disclosure and appended claims.

The term bioactive peptide compositions as used herein is intended todefine a composition consisting essentially of a mixture of peptideswith aromatic amino acids in N-terminal position, produced by hydrolysisof a protein source at a pH of 2-6 with pepsins from fish as thehydrolytic enzyme.

The bioactive peptide product of this invention is prepared by a processcomprising the steps of:

(a) hydrolyzing a selected protein material, dispersed in an aqueousmedium, together with cod pepsin at a controlled temperature and acidicpH;

(b) removing lipids and solids from the pepsin treated acidized proteinsource; and thereafter

(c) recovering the resulting bioactive peptide.

The process may employ protein material from any of a great variety ofsources including meats, fish and plants. Protein material from fish isparticularly preferred for use in the process of this invention.

The process of this invention is particularly adapted to effectingprotein hydrolysis in an acidic medium of controlled pH to produce abioactive peptide composition suitable for use in the enhancement ofgrowth of host animals. Protein material is prepared for treatment bygrinding, comminution, or other means to provide a suitable particlesize for slurring with acid. The aqueous slurry is heated with agitationat a combination of temperature and time such that the initial reactionvelocity of hydrolysis is maximized.

The enzyme employed in the process of this invention is the proteolyticpepsin enzyme derived from the stomach of Atlantic cod. In one presentlypreferred embodiment of this invention the enzyme is obtained by aprocess which comprises homogenizing the cod stomach in the presence ofenough formic acid to lower the pH to 4 and then heating for a period oftime whereby the homogenate becomes a liquid slurry due to the digestionof the tissues by the enzymes present in the stomach and thereafterrecovering from the aqueous phase following removal of sludge and oilsfollowing concentration and drying the desired pepsin enzyme.

In carrying out the process, the homogenate of the Atlantic cod stomachcan also be employed as the enzyme source. Thus following thehomogenizing of the cod stomach in the presence of acid and thedigestion of the tissues thereof by the enzymes present therein, theresulting liquid slurry which is enzyme rich can be employed directlyinto the process of the present invention as the enzyme source for theproduction of bioactive peptides.

In the production of the bioactive peptide composition of the invention,a suitable protein source is treated at a pH in the range of about 2-6,preferably at a pH of 4, with the pepsin enzyme derived from theAtlantic cod stomachs for a time to effect hydrolysis of the proteinsource so as to form a mixture of peptides having aromatic amino acidsin N-terminal positions which following heating and thereafter removalof oils and sludge provided a liquid composition consisting essentiallyof bioactive peptides and deactivated cod pepsin.

The hydrolysis step is conducted in a continuous stirred-tank reactoremploying an enzyme to protein substrate ratio selected to obtain thedesired level of conversion within a time period of 24 to 100 hours.

Generally the enzyme is added in amounts in the range of 0.5 to 5 g per1000 kg of protein.

Acid employed in the hydrolysis process in an amount to provide normally3% volume by volume.

Following the removal of oils and undissolved solids from the partiallyhydrolyzed aqueous protein material dispersion, the recovered proteinhydrolyzate fraction may be concentrated, as by reverse osmosis orthermal evaporation and dried, as by freeze drying or spray drying, andsent to product storage for subsequent packaging and distribution.

Pepsin enzyme suitable for use in one embodiment of the presentinvention is obtained by hydrolysis of Atlantic cod fish stomachs at apH in the range of 2-6. Following hydrolysis, the resulting hydrolyzateis subjected to lipid and solids removal followed by ultrafiltration ofthe resulting liquid peptide pepsin mixture to effect recovery of thepepsin enzyme therefrom.

The Atlantic cod pepsin which is used in the process of this inventionis a proteolytic enzyme prepared from Atlantic cod (Gadus morhua)stomach by autolysis. The enzyme has a specific activity of 100-200Anson Units expressed as μmol TCA-soluble tyrosine released fromhaemoglobin per hour at pH 3 and 25° C.

The compositions produced by the process of this invention have beenfound to possess significantly distinctive properties. Such compositionsare bioactive peptides which are capable of enhancing growth whenincluded in feed compositions for host animals.

Accordingly, the bioactive peptides of this invention are mostappropriate for providing a process for the enhancement of growth of ananimal by feeding such animal with an amount of such bioactive peptideto effect growth enhancement of the host animal. In general such growthenhancement is achieved when the bioactive peptide is introduced intothe host animal in an amount in the range of 0.1 to 5 g/kg body weightper day.

Feed formulations using the active peptide compositions of thisinvention will be added to conventional feed ingredients for theintended host animal an amount of bioactive peptide which is sufficientto achieve growth enhancement activity.

Generally such amounts will be in the range of from about 0.1 to about 5weight percent of the total feed, preferably from about 1 to 2%.

Enzyme hydrolysis of the protein source is normally carried out at atemperature in the range of about 10° C. to about 45° C. and at a pH inthe range of about 2 to about 6. Suitable pH is achieved by use ofeither a mineral or organic acid or salts thereof which is added priorto addition of the pepsin. The amount of acid employed is that whichwill provide the desired pH level.

In one presently preferred embodiment of the invention there is employeda lower carboxylic acid namely formic acid.

By Protein source starting materials suitable for the process of thepresent invention are:

1. fish wastes including whole trash fish, fish left after filleting,fish solubles, fish viscera and any other materials which areby-products of the fishing industry and processing

2. pork skins and tissues

3. beef tissue

4. soy bean proteins or other seed proteins

5. milk proteins

The following examples will further illustrate the process and productsof the invention.

EXAMPLE I Enzyme Preparation

Fish stomachs of Atlantic cod, collected from processing plants, arehomogenized in the presence of enough formic acid to lower the pH of thehomogenate to 4. The homogenate is then heated to 27° C. and held atthis temperature for 48 hours. During this period the homogenate becomesa liquid slurry due to digestion of the tissues by the enzymes presentin the stomachs. The liquid slurry is then stored in a tank wherein asludge gradually deposits at the bottom and oil floats to the surface.The aqueous phase between the sludge and the oil layer is thenconcentrated by ultrafiltration (cut off 10,000 mw) and sprayed dried ata temperature below the inactivation temperature for the pepsin enzyme(65° C.). The resulting dried and yellow powder contains 100-200 Ansonunits of protease activity as measured by standard assays for pepsinactivity e.g. μmol tyrosine released from haemoglobin per hour at pH 3and 25° C.

EXAMPLE II Production of Liquid Bioactive Peptides

1000 Kg of by-product from fish processing, e.g. residual meat on backbones, skins, guts, heads, were homogenized in an industrial meatgrinder and 30 liters of 85% formic acid added when the homogenate waspumped into a storage tank with stirring equipment.

To the resulting acidized homogenate was added 1 kg of cod stomachenzymes which was obtained in accordance with the protocol of Example I.The resulting mixture was then maintained at 30° C. for a period ofabout 5 days to achieve enzymatic degradation of the acidized byproducts.

Thereafter, the resulting digest was heated to a temperature of 80° C.to inactivate the added enzyme and to permit oil which was present inthe raw materials to float to the surface for removal. After removal ofoil by centrifugation in an industrial centrifuge and removal ofundissolved bones by screening there was obtained 850-950 liters of anaqueous slurry which was then concentrated by evaporation to 40% dryweight and a final volume of 250-350 liters.

The resulting concentrated product containing 20% by weight of nondigested protein and 70 weight percent of peptide and 10% minerals isdesignated liquid crude peptide product or <<LCP>>.

EXAMPLE III Production of Dried Bioactive Peptide

100 liters of the liquid crude peptide product of Example II was driedby spray drying in a NIRO spray dryer at an air out temperature of 80°C., to provide 40 kg of dried crude peptide product <<DCP>> containingundigested protein, peptides and amino acids.

EXAMPLE IV Production of Refined Peptides <<RBP>>

400 liters of LCP produced as described in Example II was subjected toconventional particle filtration using a bag filtration unit, to provideabout 250 liters of a solution free of particles bigger than 40μ.Thereafter the resulting filtrate was subjected to ultrafiltration in anindustrial hollow fiber cartridge (Amicon) filtration unit with a cutoff of 10,000 MW to provide 200 liters of a permeate containing peptideswith MW lower than 10,000. The resulting Refined Bioactive Peptide<<RBP>> can be used in the liquid form. However, 200 liters of RBP wasdried by spray drying in a Niro dryer at 85° C. (air out) to provide 80kg of RBP in dry form.

EXAMPLE V Preparation of Feed Compositions

Using dried refined peptide product as produced in Example IV, a seriesof test feed compositions were prepared using a standard dietformulation having the peptide content as noted in the following table.For performance evaluation a further series of feed compositions wasprepared in the same manner with porcine plasma protein.

Composition No. 1 2 3 4 5 6 7 Feeding Period 0-13 days Plasma protein %0 4 3 2 1 0 0 Refined Peptide % 0 0 1 2 3 4 2 Feeding Period 13-33 daysPlasma protein % 0 0 0 0 0 0 0 Refined Peptide % 0 0 0 0 0 2 1

EXAMPLE VI The Effect of RBP and Porcine Plasma Protein

To determine the effect of peptide (RBP)and porcine plasma on growthperformance of starter pigs a series of treatments using theformulations of Example V were carried out with 7 pens of 22 individualstarter pigs.

The results of the feeding treatments are shown in the following table:

Treatment composition 1 2 3 4 5 6 7 Weight (kg) Initial 5.91 5.90 5.915.91 5.91 5.91 5.91 Day 13 7.58 8.18 8.53 8.29 9.17 8.94 8.23 Day 3316.24 16.24 17.04 16.85 17.94 16.49 17.8 Weight Gain (kg) 0-13 days 1.672.28 2.62 2.37 3.26 3.03 2.32 0-33 days 10.33 10.34 11.13 10.94 12.0310.58 11.89 Weight Gain (%) 0-13 days 23 38 44 40 55 51 39 0-33 days 175175 188 185 204 179 201 Protein consumed/ 0.32 0.27 0.27 0.29 0.26 0.260.27 weight gain

The above results show that use of the bioactive peptide of the presentinvention has a marked effect on growth of young pigs and that thisproduct can replace plasma proteins in starter diets. At a level of 2%in the starter diets the bioactive peptide (RBP) causes the sameenhancement of growth as 4% porcine plasma protein during the first 13days after weaning.

Unlike plasma protein, the bioactive peptide of the present inventionresults in enhanced growth throughout the entire growth period fromweaning of the pigs and the following 33 days.

EXAMPLE VII Preparation of Fish Feed Compositions

A composition for use as a feed for salmon was prepared by admixing thefollowing ingredients:

Ingredient % of dry weight Fish Meal (low temperature dried) 44 Fishmeal (normal qualityy 19 Fish oil 20 Wheat meal 14 Potato starch 2Vitamin C 0.1 Premix (minerals and vitamins) 1.0 Carrophyll pink(astaxanthin) 0.1 Chemical composition Dry matter 96% Protein 52% Lipid21% Minerals 10%

For demonstration of the effectiveness of bioactive peptide in thesalmon feed, a composition was prepared wherein 5% of the fish meal wasreplaced by 5% of dried bioactive crude peptide (DCP ).

EXAMPLE VIII Effect of DCP on Salmon Growth

Salmon (Salmo salar) at an average individual weight of 600 grams wereseparated in two net cages in the sea with 100 fish in each cage. Onegroup was fed the standard salmon feed of Example VII and the othergroup the same feed containing 5% DCP.

After feeding for 6 months the salmon fed the standard salmon feed hadan average weight of 2.280 kg whereas the salmon fed the 5% DCP diet hadan average weight of 2.630 kg. The growth in the reference group duringthis feeding period was in other words from an average individual weightof 600 grams to 2,280g, or 1,680 grams whereas the DCP containing groupgrew from 600 grams to 2,630 grams, or 2,030 grams.

Comparison of the growth of the two groups indicates that using theproduct of the present invention there was achieved a 12% growth overthose fishes that did not receive the bioactive peptide (DCP).

We claim:
 1. A process for production of bioactive peptide compositionsthat enhance the growth of animals and fish which comprises: a. treatinga fish protein source with an acid; b. contacting the resulting acidtreated fish protein source with pepsin enzyme obtained from the stomachof Atlantic cod under conditions effecting the formation of bioactivepeptide having aromatic amino acids in the N-terminal position; c.removing lipids from the pepsin treated acidized fish protein source; d.removing solids from the pepsin treated protein source; and e.recovering the resulting bioactive peptide compositions that enhance thegrowth of animals and fish.
 2. The process of claim 1 wherein step (a)is carried out at a pH in the range of 2-6, a temperature in the rangeof 10° C. to 60° C. and for a time sufficient to effect peptideformation.
 3. The process of claim 1 wherein said aromatic amino acidsis selected from the group consisting of tyrosine, phenylalanine andarginine.
 4. The process of claim 1 wherein said acid is a mineral ororganic acid or salts thereof.
 5. The process of claim 4 wherein saidmineral acid is selected from the group consisting of hydrochloric,phosphoric and sulphuric acids.
 6. The process of claim 4 wherein saidacid is an organic acid selected from the group consisting of formic,acetic, propionic and citric acids.
 7. A process for the production ofgrowth enhancing peptide, which comprises the steps of enzymaticallyhydrolyzing a fish protein source with pepsin enzyme obtained from thestomach of Atlantic cod at a pH range of about 2 to 6 and underconditions effecting the formation of bioactive peptide having aromaticamino acids in the N-terminal position and thereby obtaining the growthenhancing peptide.
 8. The process of claim 7 wherein the enzymaticobtained peptide is recovered as a product of the process.
 9. Theprocess of claim 7 wherein said enzyme hydrolysis is carried out for aperiod in the range of 24 to 100 hours.
 10. The process of claim 9wherein said hydrolyzing is carried out at a temperature in the range offrom 10° C. to 60° C.